The Compressibility of and an Equation of State for ... - ACS Publications

James A. Beattie, Henry G. Ingersoll, Walter H. Stockmayer. J. Am. Chem. Soc. , 1942, 64 (3), pp 548–550. DOI: 10.1021/ja01255a022. Publication Date...
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J. A. BEATTIE,H. G. INGERSOLL AND W. H. STOCKMAYFCR

548

VOl. 64

Summary

Table IV the critical constants obtained in this investigation are compared with the results of other workers. The agreement of our values with those of Benedict,6who used the disappearance of the meniscus method, is striking.

The vapor pressure of isobutene was measured from 30 to 125'. The equation loglo p(atm.) = 4.37592 - (1163.34/T) represents the results well and also computes a vapor pressure at 0' in good TABLE IV agreement with that measured by Lamb and COMPARISON OF TBE CRITICAL CONSTANTS OF ISOBUTENE Roper. FROM THIS INVESTIGATION WITH THE VALUESOF OTHER The critical constants of isobutene determined AUTHORS by the compressibility method are: t, = 144.73 * $,(normal Source lo, OC. (Int.) atm,) do (g./ccJ 0.05"C. (Int.); p, = 39.48 * 0.05 normal atmosThis investigation 144.73A0.05 39.4810.05 0.234t0.002 Coffin and Maass* 143.5 phere; v, = 0.240 liter/mole (4.28 cc./g.); d, = Scheeline and Gilli4.17 mole/liter (0.234 g./cc.). The uncertainty in land4 148.9 39.7 the critical volume and density is 1%. The M.Benedicta 144.6*0.6 39.5A0.2 critical pressure and temperature given above are The prosecution of this work was greatly aided in excellent agreement with those determined by by a fellowship from the Polymerization Process Corporation. We wish to thank the M. W. Kel- Benedict, who used the disappearance of the meniscus method. logg Company for the gift of the isobutene. CAMBRIDGE, MASS.

(6) Manson Benedict, private communication.

[CONTRIBUTION FROM

THE &SEARCH

RECEIVED SEPTEMBER 25, 1941

LABORATORY OF PHYSICAL CHEMISTRY, MASSACHUSETTS INSTITUTE OF TECHNOLOGY, N O .

4891

The Compressibility of and an Equation of State for Gaseous Isobutene BY JAMES A. BEATTIE,HENRY G. INGERSOLL AND WALTER H. STOCKMAYER In earlier papers from this laboratory' the compressibilities of methane, ethane, propane, n-butane, and n-heptane have been reported. The properties of the last four substances have been measured in the same compressibility apparatus which has been described elsewhere.2 We have determined vapor pressures and critical constants of isobutene using a bomb with the glass liner.2 The compressibility of the same isobutene sample was then measured from 150 to 275' and to densities of 1.5 to 2 times the critical. The rate of polymerization of isobutene in a glass-lined bomb above 330' has been measured by Krauze, Nemtzov and Soskina.a Calculations made from their equations extrapolated to lower temperatures showed that in the time required for a complete compressibility run a t one temperature-about ten hours-the effect of the polymerization a t 225O would be of the order of the reproducibility of the compressibility measurements. Actually we measured the 250 and 275' (1) For the last report on this work see J. A. Beattie, G.-J. Su, and G. L. Simard, Tms JOURNAL, 61,926-927(1939). (2) J. A. Beattie, Proc. Am. Aced. Arts Sci., 69, 389-405 (1934). (8) M. V. Krauee, M. S. Nemtzov and E. A. Seskina, J . Gcn. Chcm., 6, 382-887 (1986).

isotherms before the effect of the polymerization became serious. As with the other hydrocarbons we measured the pressure along each isotherm from the lowest to the highest density and then repeated some of the measurements a t the lower densities as the pressure was decreased. In Table I are given the pressures for the lowest density-1 mole/liter-before and after each set of isotherms as well as the pressure a t 150' before and after the complete series of runs. It will be seen that up to 250' the effect of polymerization is small, while a t 275' it may have affected the results by as much as 0.5%. The constants of the Beattie-Bridgeman equation of state for isobutene determined from the compressibility measurements up to the critical density (4.17 mole/liter) are given in Table I1 and a comparison of the calculated with the observed pressures in Table 111. The variation of the G constant of the equation of state with density, which has been noticed for other substances, is quite evident in the case of isobutene. The change in curvature of the isometrics from negative a t low density to positive a t high density takes place a t a density between 3.5 to 4.0 mole/

COMPRESSIBILITY AND EQUATION OF STATE FOR ISOBUTENE

March, 1942

549

TABLEI EFFECT OF POLYMERIZATION OF ISOBUTENE ON THE COMpRESSIBILITY MEASUREMENTS All values are for a density of 1 mole/liter Temp., 'C.

150

175

200

225

250

275

150

36.298 36.284 0.04

38.836 38.764 0.19

25.668 25.573" 0.37

Pressure, normal atmospheres

Before isotherm 25.668 After isotherm 25.662 AP% 0.02 a After the 275' isotherm.

28.407 28.409 -0.01

-

31.087 31.083 0.01

33.713 33.707 0.02

TABLE I1

variation of A , have produced a new equation of represents the compressibility of hydrocarbons to twice the density. CHz The relation of the second virial coefficient B, P [RT(l e ) / V z ] [ V B] - A / V z - a / B~ Bo(l - b / V ) E = c / v T s to intermolecular forces has been the subject of M~I. many investigations.6 The parameter Bv is deAo a Bo b G wt. fined by the relation normal atmosphere, liter per mole, "K. ( T " K . = 1 O C . $

VALUES OF THE CONSTANTS OF THE BEATTIE-BRIDGEMAN state that EQUATION OF STATE FOR GASEOUSISOBUTENE, (CHJ)&= my..

-

A = R Units:

+

E

273.13) 0.08206 16.9600 0.10860 0.24200 0.08750 250x10' 56.0616

TABLE I11 EQUATION OF STATE WITH THE OBSERVED PRESSURES FOR GASEOUS ISOBUTENE For each temperature the fist line gives the observed pressure and the second gives the observed minus the calculated pressure. The calculated pressures are computed from the equation given in Table 11. The critical constants of isobutene are: to = 144.73OC. (Int.), pa = 39.48 normal atmosphere, u, = 0.240 liter/mole, do = 4.17 mole/liter. COMPARISON OF THE PRESSURES CALCULATED FROM TEE

Density, mole/liter Temp., 'C. (Int.) 150 obsd. obsd. calcd. 175 obsd. obsd. calcd. 200 obsd. obsd. calcd. 225 obsd. obsd. calcd. 250 obsd. obsd. calcd.

-

-

275

obsd. obsd. - calcd.

Av. dev. (atm.) Av. % dev.

1.0

1.5

2.0

2.5

3.0

3.5

4.0

4.5

5.0

6.0

7.0

8.0

43.19

43.78

47.86

61.58

65.33

78.60 111.26 189.42

80.48

87.78 110.55 157.54

9.0

Pressure, normal atmospheres

25.67 -0.20 28.41 -0.12 31.09 -0.07 33.71 -0.07 36.30 -0.08 38.84 -0.12 0.11 0.36

32.92 -0.25 37.49 -0.10 41.88 -0.07 46.24 -0.02 50.48 -0.06 54.64 -0.14 0.11 0.27

37.51 -0.15 44.14 +0.05 50.52 $0.10 56.76 $0.10 62.86 $0.02 68.86 -0.11 0.09 0.18

40.19 $0.12 49.02 +0.26 57.53 $0.25 65.88 +0.22 74.06 $0.13

41.62 41.84 42.80 +0.42 -0.02 -0.13 52.74 55.78 58.58 $0.38 $0.10 -0.96 63.52 68.99 74.43 $0.25 -0.13 -1.22 74.14 82.11 90.39 $0.19 -0.16 -0.96 84.61 95.14 106.26 $0.14 -0.03 -0.47 94.98 122.03 +O. 14 $0.19 0.20 0.25 0.09 0.66 0.35 0.45 0.13 0.88 Total average deviation (atm.), 0.218; total average

65.66 122.27 254.09

99.57 110.58 143.20 204.70 118.76 133.63 176.16 156.56 209.07

% deviation, 0.380.

liter, considerably below the critical, as is to be We have determined Bv for isobutene from plots expected. Benedict, Webb and RubinJ4by ex- of our experimental data. These are given in pressing t as a function of density by use of two Table IV. new constants and introducing a third new conWe thank the M. W. Kellogg Company and stant to express more accurately the density Dr. Manson Benedict for the gift of the pure sample of isobutene, and the Polymerization TABLE IV VALUESOF THE SECOND VIRIALCOEFFICIENTS OF GASEOUS Process Corporation for a fellowship which ISOBUTENE DETERMINED FROM THE EXPERIMENTAL DATA greatly aided this investigation. B, = Lim I) (T = constant) 1/v+o RT Summary

~(p"-

Temp.,

OC.

150 175 200 225 250 275

(Int.)

Bv, liter/mole

-0.2920 .2576 - .2260 .I988 .1760 .1568

-

-

-

(4) M. Benedict, G. B. Webb and L. C. Rubin, J . Chcm. Phys., 8 , 83444s (1940).

Measurements of the compressibility of gaseous isobutene, (CH&C=CH2, are reported from 150 to 275' and from a density of 1.0 to 9.0 mole/liter, the maximum pressure being 250 atm. In a glass-lined bomb isobutene did not poly(5) See J. A. Beattie and W. H. Stockmayer, Reports on Progress in Physics, 1, 196-229 (1940).

550

HERSCHEL H.CUDDWITH W. A. FELSING

merjze seriously during a ten-hour period until 275‘ was reached. The constants of an equation of state of gaseous isobutene were determined from the data up

Vol. 64

to the critical density; and the values of the second virial coefficients determined from the experimental data are given from 150 to 275’. RECEIVEDSEPTEMBER 25, 1941

CAMBRIDGE, MASS.

________ [CONTRIBUTION FROM THE DEPARTMENT O F CHEMISTRY, THE UNIVERSITY OF TEXAS]

Activity Coefficients of Rubidium and Cesium Sulfates in Aqueous Solution at 2501 BY HERSCHEL H. C U D DWITH ~ W. A. FELSING Introduction In a previous paper3 an experimental modification of the isopiestic method of determining activities of electrolytes was presented. In order to test the apparatus and technique still further and to gain information on the activity coefficients of two of the rarer alkali sulfates, rubidium and cesium, this investigation was undertaken. No data on the activity coefficients for these salts were found in the literature.

Experimental Method and Apparatus.-The method employed was the familiar isopiestic method, using the apparatus described by Phillips, Watson and Felsing.a The procedure in this investigation differed only in the simultaneous use of 12 solution cups instead of the usual nine; this lengthened considerably the time required for vapor pressure equilibration. Sodium sulfate was selected as the reference salt. Puri5cation of Materials. Sodium Sulfate.-The salt was crystallized four times as the decahydrate and was dehydrated according to the procedure of Ephraim.’ The mass was finally dried at 140°, ground to a fine powder, and re-dried in a vacuum oven at 140’ for seventy-two hours. It was stored in a desiccator over Anhydrone. Rubidium and Cesium Sulfates.-C. P. samples of these salts were purified wording to the directions of Archibald.s In addition, each salt was recrystallized twice from conductivity water, dried, and stored over Anhydrone. Water.-All water used had a specific conductance of 0.6-0.7 X reciprocal ohms as delivered from the still; as used, its conductance was approximately 1 X 10-6 mhos. Preparation of Solutions.-The dry salts were weighed directly from weighing bottles into weight burets by difference. To the weight buret and its contents was added a calculated amount of water. (1) Constructed from a portion of a thesis presented to the Graduate Faculty of the University of Texas by Herschel H. Cudd in partial fulfillment of the requirements for the degree of Doctor of Philosophy, June 1941. (2) Present address: E. I . du Pont de Nemours & Co., Buffalo, N.

Y.

(3) Phillips, Watson and Felsing, THIS J o u i t ~ uW, , 244 (1942) (4) Bphraim, “Textbook of Inorganic Chemistry’’ (translated by Thorne), Gurney and Jackson, London, 1934. (6) Archibald, “Preparation of Pure Inorganic Substances,” John Wiley and Sons, New York. N . Y., 193%

The solutions were weighed from the weight burets directly into the tared solution cups; the weights were checked by weighing the cups and their contents. The precision in weighing was better than one part in 5000, varying with the size of sample; samples ranged from 1.5 to 6.0 g.

The Data Obtained The isopiestic solutions investigated extended over the concentration range of approximately 0.4 to 1.9 molal. The upper limit was determined by the solubility of rubidium sulfate; the lower limit, as a practical matter, was determined by the times required for the attainment of equilibrium. The data are listed in Table I. The columns M(obs.) - M(ca1cd.) are the differences between observed values and values calculated from the smoothed curve. TABLE I MOLALITIES OF SoLUTIONS OF RUBIDIUM AND CESIUM SULFATES ISOPIESTIC WITH SOLUTIONS OF SODIUM SULFATE AT

Sodium sulfate

-

0.433 .612

0.422 .601

.780 .916

.748 .858 .968 1.118

1.031

1.198 1.488 1.610 1.716 1.800 1.875

25’

Rubidium sulfate M(0bs.) M(calcd.) M(obs.)

1.383

1.486 1.570 1.640 1.707

+0.002

+ .017 + ,008 *

.005 .OW

f

.OOO

+ ,014 + .010 + .003

Cesium sulfate M(obs.) M (calcd.)

-

M (obs.)

0.418 .565 ,715 .811 .923 1.068 1.303

1.412 1.488

-

.002

1.563

=t

.OOO

1.631

+0.006

*

,000

-

.OM

+ .003

* .OW

+ .007 * .OOO + .008 - .002 + .003

+ .008

Treatment of Results From the observed isopiestic molalities there was determined for each salt the isopiestic ratio, M(Na2S04)/M(RbS04) and M(Na$304)/ M(CszSO4). These ratios were then plotted against the observed molalities of rubidium and cesium sulfate. From the smooth curve (passing to the origin), there were read off values of the isopiestic ratio at rounded values of the molalities